Technical Field
This invention relates to a single-type solid preparation of
iodophor to be dissolved before use. This solid
preparation of iodophor is excellently stable without
releasing iodine during storage, can rapidly be dissolved in
water before use, and has various other advantages by
using the solid preparation, not liquid preparation (easy to
handle, not bulky, not in danger of liquid leakage during
transportation, etc.). Thus, it is very useful as an
iodine-type bactericide/disinfectant.
Background Art
Iodine-type disinfectants exert their bactericidal effects
under an acidic condition through iodine released. Iodine
is only slightly soluble in water and has a sublimate
property. Therefore, it is difficult to obtain a stable
preparation of iodine by merely mixing solid iodine and
solid surfactants. Then, it has been proposed that a
mixture of iodides, oxidizing agents, and acids is dissolved
in water to release iodine by chemical reaction in water.
Among the above components, a solid iodide and an
oxidizing agent lie stably in the mixture of the two.
However, once a powdered acid is added to the mixture
under the ordinary handling condition, chemical reactions
proceed gradually, and release sublimating iodine. Thus,
the stability of the preparation is seriously deteriorated.
For this reason, a 'twin-type' of solid preparation of
iodophor has been disclosed Japanese Unexamined Patent
Publication No. 2-110. In this case, two separate
preparations are prepared: one contains acids which
interfere with the stability of the preparation and the
other contains iodides and oxidizing agents, and these two
preparations are mixed before use to be dissolved.
However, it has some disadvantages of the 'twin-type'
including inconvenience for use, poor solubility, etc.
Therefore, it has earnestly been desired that not a
'twin-type' but a 'single-type' of the solid preparation of
iodophor which has excellent stability and increased
solubility is provided.
Disclosure of the Invention
The present invention was made in consideration of the
above circumstances, and it is an object of the present
invention to provide a 'single-type' solid preparation of
iodophor which is stable under the ordinary storage
conditions without releasing iodine and can easily be
dissolved before use. It is a further object of the present
invention to provide an efficient method for manufacturing
the inventive preparation of iodophor.
The inventive solid preparation of iodophor that was able
to achieve the above objects is characterized in containing:
(a) dextrin, (b) iodides (c) oxidizing agents, and (d) acids.
In this preparation, the following is preferred modes of the
present invention: the content of (a) dextrin, (b) iodides,
(c) oxidizing agents, and (d) acids in the solid preparation
of iodophor is 10 to 95%, 10 to 50%, 2 to 10%, and 5 to 50%,
respectively; and a solid preparation of iodophor which
contains potassium iodide as an iodide and potassium
iodate as an oxidizing agent in a weight ratio of 4 or
more : 1.
The methods for manufacturing the inventive solid
preparation of iodophor that was able to achieve the above
objects is the methods for manufacturing the solid
preparation of iodophor containing (a) dextrin, (b) iodides,
(c) oxidizing agents and (d) acids, which is characterized
in
granulating the dextrin (a) and at least one component
selected from the group consisting of iodides (b), oxidizing
agents (c), and acids (d) under a wet condition produced by
spraying water, powdering the resultant mixed granulated product, and mixing the powder product, if necessary, with at least
one component selected from the group consisting of
dextrin (a), iodides (b), oxidizing agents (c), and acids (d).
In the above method, the following are preferred modes of
the present invention:
the method includes granulating the dextrin (a),
together with iodides (b) and oxidizing agents (c) under a
wet condition produced by spraying water, powdering the resultant mixed granulated product, and mixing the powder product with acids (d); and/or the method includes granulating the dextrin (a),
together with iodides (b) and/or oxidizing agents (c) under
a wet condition produced by spraying water, powdering the resultant mixed granulated product, and mixing the powder product with acids (d) and, in
addition, at least one component selected from the group
consisting of dextrin (a), iodides (b), and oxidizing agents
(c), if necessary.
In the above method, the following is also preferred of the
present invention:
the content of (a) dextrin, (b) iodides, (c) oxidizing
agents, and (d) acids in the solid preparations of iodophor
is 10 to 95 %, 10 to 50 %, 2 to 10 %, and 5 to 50 %,
respectively, by weight; and/or the preparation contains potassium iodide as the (b)
iodide and potassium iodate as the (c) oxidizing agent in a
weight ratio of 4 or more:1.
In addition, it is preferred that the granulating step under
a wet condition includes granulating at a temperature of
intake air ranging from a room temperature to 120°C.
Furthermore, a solid preparations of iodophor that is a
granulated powder containing povidone-iodide and dextrin,
is included within the present invention.
In the above preparation,the following is preferred that:
the content of available iodine in the solid preparations of
iodophor is 0.005 w/w% or more;and/or the preparation contains the povidone-iodine and dextrin
in a weight ratio of 90:10 to 5:95.
The above method for manufacturing solid preparations of
iodophor is characterized in that the povidone-iodine and
dextrin are granulated under a wet condition produced by
spraying water. In the method, it is preferred that the
granulated powder is obtained at a temperature of intake
air ranging from a room temperature to 120°C.
Brief Description of the Drawings
FIG. 1 shows a schematic diagram of the fluid bed
granulation dryer used in the present invention.
Description of the symbols
1. Powdered raw material
2. Liquid delivery pump
3. Spray nozzle
4. Bag filter
Best Mode for Carrying Out The Invention
Considering the easiness of handling, etc., and paying
attention to the 'single-type solid preparation of iodophor',
the inventors have intensively investigated about
increasing the stability and solubility of the solid
preparation of iodophor. Therefore, they found that when
dextrin is used as the iodine carrier, iodides and oxidizing
agents can stably be retained in the dextrin without
releasing iodine during storage, and that when water is
sprayed on each component of the above preparation [the
above (a) and at least one of (b), (c) and (d)] and when a
liquid bed granulation dryer (for example, "Flow Coater
Model FLO-5B" manufactured by Okawara Seisakusho,
abbreviated as " "Flow Coater" hereinafter) is used for the
preparation of the solid preparation, a desired solid
preparation of iodophor with excellent stability and
solubility can be provided, they accomplished the
invention.
The most prominent features of the present invention are
the use of dextrin as the iodine carrier as well as the
water spraying on each component or their mixture during
the granulatin and mixing process.
A 'single-type' of solid preparation of iodophor, which
contains both polyvinylpyrrolidone (PVP) and dextrin as
carriers as well as iodine and iodides, has also been
disclosed heretofore Japanese Unexamined Patent
Publication No. 9-100234. According to the above
publication, however, there is a recognition that "dextrin,
by itself alone, cannot lead to the formation of an
excellently stable iodine complex". Accordingly, those
inventors contemplated improvements of stability by
mixing PVP or poly-N-vinylcaprolactam as an iodine
carrier in addition with dextrin.
On the contrary, the present invention is clearly and
constitutionally different from the invention disclosed in
the above publication in that dextrin alone is used as the
iodine carrier, and that PVP is not essentially contained.
Although it has been believed, according to the above
publication, that "when dextrin alone, without PVP, is
used, an excellently stable iodine complex cannot be
obtained", the manufacturing methods described in the
present invention could unexpectedly provide an
excellently stable iodophor preparation without releasing
iodine during storage even when dextrin alone is used.
This point carries the technical significance of the present
invention.
The above methods of the present invention, that is, the
method for preparation by spraying water on each
component constituting the solid preparation of iodophor
or their mixture and by using a liquid bed granulation
dryer (Flow Coater), etc., has been found to be also
extremely valid for manufacturing preparations comprising
a povidone-iodine containing PVP and dextrin. Thus, it
was shown that the granulated powder preparations
containg povidone-iodine and dextrin prepared by the
above manufacturing methods increase remarkably in
water solubility and improve significantly in the
bactericidal/disinfectant effect.
In the following, each component constituting the present
invention is described.
First of all, solid preparations of iodophor which contain
(a) dextrin, (b) iodides, (c) oxidizing agents, and (d) acids
are described.
(a) Dextrin
Dextrin is very important in the present invention as the
component carrying iodine. Dextrin is obtained by
hydrolyzing starch with an enzyme or acid, but
commercially available products such as calcined dextrin
and saccharified dextrin may be utilized.
For more effective exertion of the above carrier effect, the
use of cyclodextrin or porous dextrin is preferred.
(b) Iodides
There is no special restriction on the iodides to be used
except that they must dissociate in the aqueous solution to
release iodide ions. The examples of such iodides include
alkaline metal iodides (sodium iodide, potassium iodide,
etc.) and alkaline earth metal iodides (calcium iodide,
magnesium iodide, etc.) as metallic iodides, and ammonium
iodide, etc. as nonmetallic iodides. Among them, the use
of alkaline metal iodides is recommended. Iodides
obtained by reducing iodates (potassium iodate, sodium
iodate, etc.) may be used.
(c) Oxidizing agents
There is no special restriction on the oxidizing agents
except that they must generate iodine molecules by
reacting with the above iodides. The examples of such
oxidizing agents include acids such as iodic acid, bromic
acid, chromic acid, permanganic acid, peroxy acid
(peroxytitanic acid, peroxynitric acid, peroxyphosphoric
acid, etc.), iodine oxides (diiodine tetraoxide, diiodine
pentaoxide, tetraiodine nonaoxide, etc.), halogenated
isocyanuric acids (one to three hydrogens in isocyanuric
acid are substituted by halogens including chlorine, iodine,
and bromine, preferably by chlorine), etc. and their salts.
The above salts include alkaline metal salts (sodium salts,
potassium salts, etc.), alkaline earth metal salts (calcium
salts, magnesium salts, etc.), non-metal salts (ammonium
salts, amine salts, etc.), etc. Among them, alkaline metal
salts are preferred, and sodium salts and potassium salts
are more preferred.
In the concrete, the use of iodic acid, peroxy acid,
halogenated isocyanuric acids, and their salts is
recommended, and the use of iodates (sodium iodate,
potassium iodate, etc.) as well as halogenated isocyanuric
acids and their salts (sodium dichloroisocyanurate,
trichloroisocyanuric acid, etc.) is especially preferred.
(d) Acids
Acids to be used in this invention include ones, such as
powdered acids; powdered acidic acid salts; lactones,
carboxylic acid anhydrides, etc., that are soluble in water
and hydrolyzed to acidic compounds. The examples of the
powdered acids include saturated dicarboxylic acids (oxalic
acid, malonic acid, succinic acid, etc.), unsaturated
dicarboxylic acids (maleic acid, fumaric acid, etc.),
oxy-acids (malic acid, tartaric acid, citric acid, etc.),
inorganic acids (boric acid, pyrophosphoric acid,
metaphosphoric acid, phosphorous acid, etc.), etc. The
examples of the powdered acidic acid salts include acidic
salts of inorganic acids such as hydrogen alkaline metal
salts of inorganic acids (sodium dihydrogenphosphate,
sodium hydrogensulfate, etc.) Among them, oxalic acid,
citric acid, and alkaline metal hydrogensulfates (sodium
salt, etc.) are preferred. The examples of lactones include
glucono-delta-lactone, etc., and the examples of carboxylic
acid anhydrides include succinic anhydride, maleic
anhydride, etc.
The preferred content of these components in the solid
preparation of iodophor is as follows: (a) dextrin: not less
than 10% and not more than 95% (more preferably, not less
than 20% and not more than 50%), (b) iodides: not less
than 10% and not more than 50% (more preferably, not
more than 20%), (c) oxidizing agents: not less than 2% and
not more than 10% (more preferably, not more than 5%),
and (d) acids: not less than 5% and not more than 50%.
When a powdered base having an effervescent property is
to be added to the preparation, it is preferred to
appropriately adjust the amount of (d) in proportion to the
amount of the base.
When potassium iodide is used as (b) the iodide and
potassium iodate as (c) the oxidizing agent, it is
recommended for the preparation to contain potassium
iodide and potassium iodate in a weight ratio of 4 or
more:1.
The above solid preparation of iodophor contains the (a) to
(d) as essential components, and can also contain the
following components unless they deteriorate the effect of
the invention.
Powdered bases having an effervescent property in
reaction with acids
The powdered base means a powdered alkaline base
(normal salts, acid salts, etc.). It is no special
limitations to be used except that it has effervescence
preperty in reaction with the (d) acids. In the concrete,
they include carbonates (alkaline metal carbonates, etc.
including sodium carbonate, potassium carbonate,
ammonium carbonate, etc.), hydrogencarbonates (alkaline
metal hydrogencarbonates, etc. including sodium
hydrogencarbonate, potassium hydrogencarbonate,
ammonium hydrogencarbonate, etc.), etc. In particular,
the use of alkaline salts of hydrogencarbones (sodium salts,
etc.) is recommended.
Skin-protecting agents
The skin-protecting agents include ones such as hyaluronic
acid, urea, chondroitin sulfate, chitin, chitosan, collagen,
allantoin, and aloe gel as well as the following agents
powered by using β-cyclodextrin: glycerin, sorbitol,
poly(ethylene glycol), lanolin, squalene, etc.
Other components such as vapor absorbents (sodium
sulfate, potassium sulfate, etc.), binders (mannitol, etc.),
etc. may be added if necessary.
In the following, the methods of manufacturing the
preparation are described.
For manufacturing the solid preparation of iodophor
containing the (a) dextrin, (b) iodides, (c) oxidizing agents,
and (d) acids, it is required that dextrin (a) and at least
one component selected from the group consisting of
iodides (b), oxidizing agents (c), and acids (d) are
granulated under a wet condition produced by spraying
water, and that the resultant mixed granulated product
are powdered and mixed, if necessary, with at least one
component selected from the group consisting of dextrin (a),
iodides (b), oxidizing agents (c), and acids (d). In its
essence, the most important point of this manufacturing
methods lies in that the (a) and at least one component
selected from (b), (c), and (d) are sprayed with water,
followed by granulation and drying with the liquid bed
granulation dryer (Flow Coater), etc. The methods make
it possible to produce a single-type of a solid preparation
of iodophor which is very excellent in the stability without
releasing iodine during its storage and also excellent in
the solubility even when dextrin alone is used as the
carrier.
In the concrete, at first, dextrin (a) and at least one
component selected from the group consisting of iodides (b),
oxidizing agents (c), and acids (d) are granulated under a
wet condition produced by spraying water to obtain a
mixed granulated product. The resultant mixed
granulated product may occur in the following three modes
(1 ○ to 3 ○).
1 ○ Mixed granulated products containing two components,
that is, the (a) and another component selected from the
(b), (c), and (d) [namely, mixed granulated products
containing dextrin (a) and iodides (b); mixed granulated
products containing dextrin (a) and oxidizing agents (c);
and mixed granulated products containing dextrin (a) and
acids (d)]; 2 ○ Mixed granulated products containing three components,
that is, the (a) and two other components selected from (b),
(c), and (d) [namely, mixed granulated products containing
dextrin (a), iodides (b), and oxidizing agents (c); mixed
granulated products containing dextrin (a), iodides (b),
and acids (d); and mixed granulated products containing
dextrin (a), oxidizing agents (c), and acids (d)] 3 ○ Mixed granulated products containing the four
components (a), (b), (c), and (d) [namely, mixed granulated
products containing dextrin (a), iodides (b), oxidizing
agents (c), and acids (d)]
For the purpose of obtaining more excellent stability and
solubility, it is most highly recommended to granulate
iodides (b), oxidizing agents (c), and acids (d) separately,
and then mix them. When the manufacturing efficiency,
etc. are taken into consideration, however, a preferred
mode of the mixture contains dextrin (a), and iodides (b)
and/or oxidizing agents (c), and it is recommended to mix
this mixture with acids (d) later.
As for the mixing step, either is acceptable whether to
simply mix the appropriate components or to use an
appropriate reaction mixture such as the
oxidation-reduction reaction product of an iodide and an
oxidizing agent (for example, potassium iodide and
potassium iodate) as described in the below examples.
As the next step, the mixed granulated product is
powdered, and if necessary, mixed with at least one
component selected from the group consisting of dextrin (a),
iodides (b), oxidizing agents (c), and acids (d). Thus, the
desired solid preparation of iodophor is obtained. As
noted above, the inventive solid preparation contains
dextrin (a), iodides (b), oxidizing agents (c), and acids (d).
Therefore, when mode 3 ○ [a mixed granulated product
containing all four components of (a), (b), (c), and (d)] is
adopted as an example of the three modes (1 ○ to 3 ○) of mixed
granulated products, it is the only required process for
obtaining the desired solid preparation of iodophor to
powder the mixed granulated product, and it is not
essentially required to mix at least one component selected
from the group consisting of dextrin (a), iodides (b),
oxidizing agents (c), and acids (d). As a matter of course,
it is also acceptable to impose a subsequent process for
mixing at least one component selected from the group
consisting of dextrin (a), iodides (b), oxidizing agents (c),
and acids (d). In another mode, for example, in mode 2 ○ [a
mixed granulated product containing three components], it
is required, for manufacturing the inventive solid
preparation of iodophor which contains the four
components, to mix at least one component which is absent
from the previously mixed granulated product. In the
present invention, either is acceptable whether this fourth
component alone is added and mixed or is premixed with
one or more of the remaining components. The same is
applied to the mixed granulated product of mode 1 ○
containing two components. That is, for manufacturing
the desired solid preparation of iodophor containing the
four components, it is required to mix the previously mixed
granulated product with the other two components which
are absent from the previously mixed granulated product.
In another way, these two components to be mixed may be
premixed with one or two of the remaining two components.
In the present invention, the expression, "if necessary", is
used with an intention of including these various modes.
It is particularly recommended that a mixed granulated
product contains granulating dextrin (a), together with
iodides (b) and/or oxidizing agents (c), under a wet
condition produced by spraying water is powdered, mixed
with acids (d), and if necessary, further mixed with at
least one component selected from the group consisting of
dextrin (a), iodides (b), and oxidizing agents (c). It is
most recommended that a mixed granulated product
comprising wherein granulating dextrin (a), together with
iodides (b) and/or oxidizing agents (c), under a wet
condition produced by spraying water, powdering the
resultant product, and mixing the powder product with
acids (d), and if necessary, further with iodides (b) and/or
oxidizing agents (c). In this process, it is preferred to
spray water containing a binder (pullulan, gum arabic,
etc.).
In the following, the liquid bed granulation dryer (Flow
Coater) used in the present invention is described by
means of FIG. 1 (schematic diagram of the dryer).
First of all, water is introduced into the liquid delivery
pump 2, and an appropriate powdered raw materials 1 is
placed on the bottom of the Flow Coater. The water
delivered by the liquid delivery pump 2 is sprayed on the
powdered raw material 1 through the spray nozzle 3. The
Flow Coater has been equipped with the bag filter 4 to
prevent the powdered raw material 1 escaping from the
Flow Coater. The powdered raw material 1 is granulated
and dried by supplying intake air (hot air) from the bottom
of the Flow Coater to blow the powder up while water is
sprayed. Depending on the kind of the powdered raw
material, etc., the conditions of mixing, spraying, and
drying can be suitably selected within the respective
desired ranges.
Within the allowable range of the liquid bed granulation
dryer, preferred conditions of spraying and drying are as
follows.
Temperature of intake air:room temperature to 120°C
It is recommended that the lower limit of the temperature
of intake air is set at not less than room temperature,
more preferably not less than 50°C. Defining the lower
limit within this range prevents blocking of the powder
(solidification), which may occur because of insufficient
drying (spraying excess water), as well as coloration, etc.
of the powder because of released iodine, and can also
prevent the prolongation of manufacturing time and the
decreases in working efficiency. Thus, the cost rising is
prevented. Still more preferred is 80°C or more.
On the other hand, the recommended upper limit of the
temperature of intake air is 120°C or less, more preferably
100°C or less. At a temperature higher than 120°C, the
water sprayed is vaporized within a short time, and
thereby powder adsorption is delayed, causing
prolongation of manufacturing time, decreases in working
efficiency, and rising of the cost. Still more preferred is
95°C or less.
Wind delivery pressure:100 to 400 mm/Aq
The wind delivery pressure means ones to be applied to
make the powder float. It may be adjusted according to
the specific gravity or amount of the mixed powder to be
loaded, but it is preferred to define the wind delivery
pressure within the range from 100 to 400 mm/Aq. When
a pressure less than 100 mm/Aq is applied, the powder
does not float, and as a result, the water is sprayed only
on the upper portion of the loaded volume of the powder,
causing blocking (solidification), coloration, etc. of the
powder because of released iodine. Still more preferable
is 150 mm/Aq or more. At a wind delivery pressure higher
than 400 mm/Aq, the powder floats at a level higher than
the spray nozzle, so that the water cannot evenly be
sprayed on the powder, resulting in granulation failure in
some portion of the loaded volume of the powder. This
causes some unfavorable phenomena including irregularity
in particle size, etc. More preferred is 300 mm/Aq or less,
and still more preferred is 250 mm/Aq or less.
Premixing time:30 minutes or less
The premixing time means the mixing time taken for
preparing the granulated mixture. When the premixing
time is longer than 30 minutes, the difference in specific
gravity of the powder leads to insufficient mixing, lack of
uniformity of the resultant mixed granulated product. In
addition, the accompanying prolongation of manufacturing
time and the decrease in working efficiency make the cost
rise. More preferred is 10 minutes or less, and still more
preferred is 5 minutes or less. When the premixing time
is less than 2 minutes, the resulting insufficient powder
mixing causes lack of uniformity of the resultant mixed
granulated product, and water spraying on the powder that
has not sufficiently been heated causes insufficient drying,
which results in blocking of the powder (solidification) or
coloration by released iodine. Thus, the premixing time of
2 minutes or more is recommended. More preferred is 3
minutes or more.
Time for and frequency of water spraying; time for and
frequency of interim-drying; and time for finish-drying
These parameters are closely related with each other, and
also related to the temperature of the intake air. In
considering how excessively water spraying is vaporized
(interim-drying), how the water content of the mixed
granulated product can be adjusted (finish-drying),
whether the cost can be decreased by shortening total
manufacturing time, and other things, it is recommended
to adjust these parameters within the range described
below.
Time for the post-premixing process: 5 to 40 minutes
When the above process takes less than 5 minutes,
insufficient granulation causes lack of uniformity of the
resultant particle size, and desired effects cannot be
obtained because of the existence of fine particles. More
preferred is 10 minutes or more, and still more preferred
is 15 minutes or more. When the process takes more than
40 minutes, the cost rises. More preferred is 30 minutes
or less, and still more preferred in 20 minutes or less.
Amount of water to be sprayed:5 to 30 w/w% with respect
to the total weight of powdered raw material
The amount of water to be sprayed is closely related with
the below time for and frequency of spraying, and
additionally may be changed by the temperature of intake
air. When the temperature of intake air is high,
increased amounts of water can be sprayed, and the time
for spraying can be prolonged. In addition, it is also
possible to conduct a frequency of water spraying at once.
Thus, it is advisable to appropriately adjust the above
parameters so as to prevent solidification which may be
caused by an excessive content of water spraying in the
powder and coloration by released iodine, etc.
It is preferred that the total amount of water spraying is
adjust to 5 to 30 w/w% with respect to the total weight of
the powdered raw material. When the total amount of
water spraying is less than 5 w/w%, insufficient
granulation causes lack of uniformity of the resultant
particle size, and desired effects cannot be obtained
because of the existence of fine particles. More preferred
is 10 w/w% or more. However, when the total amount of
water spraying is more than 30 w/w%, prolongation of
manufacturing time, blocking (solidification) of the powder,
coloration by release of iodine, and others occur,
decreasing the working efficiency. More preferred is 20
w/w% or less, and still more preferred is 15 w/w% or less.
Time for and frequency of spraying
The time for and frequency of spraying are to be
appropriately adjusted within a appropriate range in
consideration of the time for interim-drying (as noted
below), etc. It is preferred to spray 1 to 10 times for 1 to
5 minutes each, and more preferred to spray 3 to 5 times
for 2 to 3 minutes each.
It is recommended to set the total time for spraying within
5 to 20 minutes. When the total time for water spraying
is set at less than 5 minutes, insufficient drying (an
excessive content of water spraying) occurs during
spraying, causes blocking (solidification) of the powder as
well as coloration by released iodine, leading to decreased
working efficiency. More preferred is 7 minutes or more.
However, when the total time for water spraying is too
long, insufficient granulation causes lack of uniformity of
the resultant particle size, and desired effects cannot be
obtained because of the existence of fine particles. More
preferred is 15 minutes or less.
Time for interim-drying:5 minutes or less
The interim-drying means a preliminary drying process
imposed between spraying and drying (finish-drying).
Concretely, if spraying is conducted only once in each
course of mixing → spraying → drying, then,
interim-drying is skipped, and a finish-drying process is
conducted once. However, if spraying is conducted 4 times,
interim-drying is conducted 3 times, and a finish-drying
process is conducted once at last. The interim-drying is
distinguished from the finish-drying, which is conducted in
order to appropriately adjust the water content before
finishing off the final product, by its significance that it
prevents the retainment of excessive water, derived from
water spraying, in the powder (an excessive water content
leads to solidification of the powder and coloration by
released iodine, etc.).
The above time for interim-drying can be decided according
to the frequency of spraying, etc. as noted above.
However, when the time for interim-drying is too short,
insufficient drying (an excessive content of water
spraying) leads to blocking (solidification) of the powder or
coloration by released iodine, etc., and decreases the
working efficiency. Preferred is 30 seconds or more, and
more preferred is 1 minute or more. However, when the
time for interim-drying is longer than 5 minutes,
prolongation of working time makes the cost rise, and
desired effects cannot be obtained because of insufficient
granulation which causes lack of uniformity of the
resultant particle size and the existence of fine particles.
In addition, unfavorable phenomena including
disintegration of granules occur. More preferred is 3
minutes or less, and still more preferred is 2 minutes or
less.
Time for finish-drying:10 minutes or less
The finish-drying is conducted in order to finally adjust
the water content in the mixed granulated product. Too
short finish-drying causes insufficient drying which leads
to blocking (solidification) of the powder as well as
coloration by released iodine. Preferred is 1 minute or
more, and more preferred is 2 minutes or more. However,
when the time for finish-drying is longer than 10 minutes,
prolongation of working time makes the cost rise, and
desired effects cannot be obtained because of insufficient
granulation which causes lack of uniformity of the
resultant particle size and the existence of fine particles.
In addition, unfavorable phenomena including
disintegration of granules occur. Preferred is 5 minutes
or less, and more preferred is 3 minutes or less.
It is preferred that the water content in granulated powder
obtained in this manner is 0.5 to 10 w/w%. A water
content of less than 0.5 w/w% causes easy disintegration
and poor solubility. A water content of more than 10
w/w% increases reactivity with acids, and causes iodide
release, leading to easy coloration. More preferred is 5
w/w% or less, and still more preferred is 2 w/w% or less.
The above method is also useful as a method for
manufacturing solid preparation of iodophor containing
povidone-iodine (a complex of PVP and iodine) and dextrin.
Namely, a mixture of them is sprayed with water,
granulated in the wet condition, and powdered. Thus,
iodine release is inhibited, and stability can markedly be
increased. The conditions of mixing, spraying, and drying
can appropriately be adjusted according to the mixture
ratio of povidone-iodine and dextrin, etc. The preferred
conditions are as noted above.
It has been known that povidone-iodine shows a strong
antibacterial activity against pathogenic bacteria which
infect man, animals, and plants, rapidly kills all species of
microorganisms including bacteria, viruses, molds,
spore-forming bacteria, protozoa, and yeast, and is also
effective against some species of insect, parasite, and
nematode. Povidone iodine has been widely used as a
bactericide/disinfectant for animals and as a gargle for
man, etc. because it has a strong bactericidal activity and
a broad antibacterial spectrum as mentioned above, and is
also relatively safe for the human body. For example,
aqueous solutions of povidone-iodine have been used for
various purposes including: disinfectants for barns and
devices for livestock farming (sterilization of floors, walls,
and ceilings of cow sheds, piggeries, and poultry houses;
sterilization of milking devices and incubation devices;
post-milking sterilization of nipples; sterilization of
hatching egg shells; and others); disinfectants for
machines for manufacturing foods and fermentation, etc.
(sterilization of facilities and equipment; sterilization of
storehouses and refrigerators for components and
products; sterilization of containers and packing
materials; and others); disinfectants for the wood, etc.
nematicide, antisepsis, and anti-microorganism for
imported wood; antisepsis and anti-microorganism for
leather, paste, textile, paint; and others); environmental
disinfectants (sterilization of digester chambers, septic
tanks, and water distribution pipes; sterilization of
putrefied swamps and ponds); plant disinfectants
(antisepsis, anti-microorganism, and insect control for
imported plants, tea leaves, and crude drugs; sterilization
of storehouses and refrigerators for them; and others);
disinfectants for public facilities (sterilization of toilet
facilities, wards, and filth facilities in hospitals;
pet-related environment; sterilization of the interior of
feeding facilities, theaters, public lavatories, public
bathes, and vehicles; and others); soil disinfectants;
household disinfectants; disinfectants for combs, scissors,
etc. used at barber shops/beauty salons; and others.
Thus, povidone-iodine, like molecular iodine, has a strong
antibacterial activity and a broad antibacterial spectrum,
and does not confer on microorganisms resistance for
povidone-iodine. In addition, povidone-iodine has some
advantages including less peculiar odor characteristic of
iodine, higher safety than that of halogen-type
antibacterial agents, and less irritation to humans and
animals. On the other hand, the povidone-iodine has the
problems because of its poor water solubility, a long time
(a few hours to 24 hours) is required to dissolve
povidone-iodine in water, that vigorous stirring causes
partial ionization of iodine hold in the complex and
decreases its bactericidal effect, and a low concentration
solutions of povidone-iodine loose its bactericidal effect
within a relatively short period of time.
It was found that when fine powder of such
povidone-iodine is coated/granulated with fine powder of
very highly water-soluble dextrin, its water solubility is
highly improved, and that such granulated powder of
pvidone iodine/dextrin is completely dissolved in water
within a few minutes.
The above granulated powder of povidone-iodine/dextrin is
produced by utilizing dextrin for granulating and
powdering povidone-iodine, and contains available iodine
at a concentration of at least 0.005%. In the concrete, the
povidone-iodine contains available iodine at a
concentration of 8 to 13 w/w% as PVP-iodine complex, and
the weight ratio of povidone-iodine to dextrin in the
granulated powder of povidone-iodine/dextrin is preferably
90:10 to 5:95, and especially preferably 80:20 to 10:90.
Water solubility of the povidone-iodine/dextrin powder
correlates with the amount of dextrin. Water solubility is
higher when the amount of dextrin is larger, and a 10
w/w% or lower content of dextrin makes its solubility poor.
At a 5 w/w% or lower content of povidone-iodine, however,
its bactericidal effect is deteriorated although its
solubility is excellently high. When a fine powder
prepared by simply mixing povidone-iodine and dextrin is
added in water, povidone-iodine and dextrin separate from
each other, so that povidone-iodine comes to float on the
water surface and takes a long time for dissolution.
However, when granules prepared by granulation of
povidone-iodine with dextrin are added in water, they sink
in a moment, and completely dissolve within a few
minutes.
The present invention is illustrated below in more detail
by reference to some examples. However, the following
examples do not restrict this invention, and it is all within
the contemplation of the present invention to make
modifications in the invention unless they deviate from the
above- and below tenor.
PREPARATION EXAMPLE 1
1 ○ Potassium iodate was partially reduced with hydrazine,
and the powder mixture (740 g) containing the resultant
potassium iodide and unchanged potassium iodate in a
ratio of 5:1 (by weight) was placed in Flow Coater ("Flow
Coater Model FLO-5B", Okawara Seisakusho) together
with 2 ○ dextrin powder (1260 g, trade name "pinedex #3",
Matsutani Kagaku Kogyo), sprayed with water or water
containing binders under the below conditions, and
granulated and dried, resulting in a powder (weight ratio
of 1 ○ to 2 ○ = 37:63).
[Conditions for spraying, granulating, and drying]
Temperature of intake air |
around 90°C |
Temperature of exhaust gas |
40 to 50°C |
Wind delivery pressure |
150 to 200 mm/Aq |
Time for premixing |
5 minutes |
Time for and frequency of water spraying |
2 minutes and 30 seconds each, 4 times (amount of water spraying 350 mL/4 times) |
Time for and frequency of interim-drying |
1 minute each, 3 times |
Time for finish-drying |
5 minutes |
The resultant powder was filtered, and a powder with
particle size of around 40 mesh was obtained. This
powder was mixed with citric anhydride, sodium
hydrogencarbonate, and a surfactant (sodium salt of the
condensation product between naphthalensulfonic acid and
formalin) in the following ratio:
Granulation product containing (KIO3 + KI) and dextrin | 33 w/w% |
Citric anhydride | 45 w/w% |
Sodium hydrogencarbonate | 20 w/w% |
Surfactant | 2 w/w% |
PREPARATION EXAMPLE 2
To 10% ethanol aqueous solution (1800 g), 900 g
povidone-iodine was added, and dissolved while being
heated at 40 to 50°C. On the other hand, 2100 g dextrin
fine powder ("Pinedex #6", Matsutani Kagaku Kogyo) was
added to water (3150 g), and dissolved under stirring.
Each solutions obtained in this manner were sufficiently
mixed respectively, stirred, and homogenized, and then
powdered by using a spray drier ("Spray Drier Model L-8",
Okawara Seisakusho) (time for spraying 150 minutes,
atomizer 25000 r.p.m.) to obtain 2540 g of the resultant
powder. A position of 2500 g was taken from this powder,
placed in a testing Flow Coater ("Flow Coater Model
FLO-5B", Okawara Seisakusho), sprayed with water under
the below conditions, and granulated and dried. As a
result, the desired povidone-iodine/dextrin granulated
powder was obtained.
[Conditions for spraying and granulating/drying]
Temperature of intake air |
around 90°C |
Temperature of exhaust gas |
40 to 50°C |
Wind delivery pressure |
150 mmHg |
Time for and frequency of water spraying |
2 minutes and 30 seconds each, 4 times (amount of water spraying 400 mL/4 times) |
Time for and frequency of interim-drying |
1 minute and 10 seconds each, 3 times |
Time for finish-drying |
2 minutes |
EXAMPLE 1 (Stability Test)
In this example, a stability test was performed as
described below for the purpose of confirming the excellent
stability of the inventive solid preparation of iodophor by
comparing some examples of the present invention and
reference examples obtained by simple mixing of each
component not by using the present invention.
[Example 1 of the present invention]
First of all, the granulated powder containing potassium
iodide (KI), potassium iodate (KIO3), and dextrin was
obtained in the same manner as described in the
PREPARATION EXAMPLE 1. This granulated powder was
placed in a vinyl plastic bag, and mixed with citric
anhydride and sodium hydrogencarbonate placed in the
bag.
The resultant Example 1 of the present invention
contained each component in the following weight ratio:
Granulated powder containing KI, KIO3, and dextrin | 135.63 g (38.75%) |
Citric anhydride | 148.71 g (42.49%) |
Sodium hydrogencarbonate | 65.66 g (18.76%) |
[Example 2 of the present invention]
The components were processed, granulated, and dried in
the same manner as described in PREPARATION EXAMPLE
1, except that a mixed powder containing KI and KIO
3 in a
ratio of 6:1 (by weight) was used, and obtained a powder
(ratio of 1 ○ to 2 ○ was 37:63 by weight). To this granulated
powder, citric anhydride was added in the following ratio,
and mixed.
Granulated powder containing KI, KIO3, and dextrin | 265.5 mg (72.64 %) |
Citric anhydride | 100.0 mg (27.36 %) |
[Example 3 of the present invention]
In the Examples 1 and 2 of the present invention, the
desired solid preparation of iodophor was obtained by
using mixed powders, the ratio of KI to KIO
3 in which was
modified by reduction reaction. However, in Example 3 of
the present invention, KI and KIO
3 were mixed with each
other, and the resultant mixture was used to obtain the
desired solid preparation of iodophor. Namely, 1 ○ a powder
mixture (740.7 g) containing KI and KIO
3 in a ratio of 6:1
(by weight) and 2 ○ dextrin powder (1259.3 g, trade name
"
Pinedex #3", Matsutani Kagaku Kogyo) were placed in the
Flow Coater ("Flow Coater Model FLO-5B", Okawara
Seisakusho), and sprayed with water in the same manner
as described in PREPARATION EXAMPLE 1, granulated
and dried, and a powder (weight ratio of 1 ○ to 2 ○ = 37:63) was
obtained. To this granulated powder, citric anhydride was
further added in the following ratio, and mixed.
Granulated powder containing KI, KIO3,and dextrin | 265.5 mg (72.64 %) |
Citric anhydride | 100.0 mg (27.36 %) |
[Example 4 of the present invention]
The components were processed, granulated, and dried in
the same manner as described in PREPARATION EXAMPLE
3, except that 1 ○ KI and KIO
3 in a ratio of 8:1(by weight)
were mixed with each other, and obtained a powder (ratio
of 1 ○ to 2 ○ was 37:63 by weight). To this granulated powder,
citric anhydride was further added in the following ratio,
and mixed.
Granulated powder containing KI, KIO3, and dextrin | 341.4 mg (77.34 %) |
Citric anhydride | 100.0 mg (22.66 %) |
[Example 5 of the present invention]
The components were processed, granulated, and dried in
the same manner as described in PREPARATION EXAMPLE
1, except that 1 ○ KI (740.7 g) and 2 ○ dextrin powder (1259.3
g, trade name "
Pinedex #3", Matsutani Kagaku Kogyo)
were used, and obtained a powder (ratio of 1 ○ to 2 ○ was
37:63 by weight). To this granulated powder, KIO
3,
dextrin, and citric anhydride were further added in the
following ratio, and mixed.
Granulated powder containing KI and dextrin | 227.6 mg (62.27 %) |
KIO3 | 14.0 mg ( 3.83 %) |
Dextrin | 23.9 mg ( 6.54 %) |
Citric anhydride | 100.0mg (27.36 %) |
[Example 6 of the present invention]
The components were processed, granulated, and dried in
the same manner as described in PREPARATION EXAMPLE
1, except that 1 ○ KIO
3 (740.7 g) and 2 ○ dextrin powder
(1259.3 g, trade name "
Pinedex #3", Mateutani Kagaku
Kogyo) were used, and obtained a powder (ratio of 1 ○ to 2 ○
was 37:63 by weight). To this granulated powder, KI,
dextrin, and citric anhydride were further added in the
following ratio, and mixed.
Granulated powder containing KIO3 and dextrin | 37.9mg(10.37 %) |
KI | 84.3mg (23.06 %) |
Dextrin | 143.3mg(39.21 %) |
Citric anhydride | 100.0mg(27.36 %) |
[Example 7 of the present invention]
The components were processed, granulated, and dried in
the same manner as described in PREPARATION EXAMPLE
1, except that 1 ○ citric anhydride (740.7 g) and 2 ○ dextrin
powder (1259.3 g, trade name "
Pinedex #3", Matsutani
Kagaku Kogyo) were used, and obtained a powder (ratio of
1 ○ to 2 ○ was 37:63 by weight). To this granulated powder,
KI and KIO
3 were further added in the following ratio, and
mixed.
Granulated powder containing citric anhydrid | 270.3 mg (73.31 %) |
KI | 84.3 mg (22.86 %) |
KIO3 | 14.1mg (3.82 %) |
[Example 8 of the present invention]
The components were processed, granulated, and dried in
the same manner as described in PREPARATION EXAMPLE
1, except that KI and KIO
3 were mixed in a ratio of 6:1 (by
weight), and obtained a powder (ratio of 1 ○ to 2 ○ was 37:63 by
weight). To this granulated powder, KI and citric
anhydride were further added in the following ratio, and
mixed.
Granulated powder containing KI, KIO3, and dextrin | 265.5 mg (67.45 %) |
KI | 28.1 mg (7.14 %) |
Citric anhydride | 100.0 mg (25.41 %) |
[Reference example 1]
KI, KIO3, and dextrin were simply mixed not by using Flow
Coater. The resultant powder was placed in a
widemouthed brown bottle (diameter of the mouth: about
100 mL), and citric anhydride and sodium
hydrogencarbonate were further added, and mixed.
The resultant reference example 1 contained the individual
components in the following weight ratio:
KI | 11.95 g (11.95 %) |
KIO3 | 2.39 g (2.39 %) |
Dextrin | 24.41 g (24.41 %) |
Citric anhydride | 42.49 g (42.49 %) |
Sodium hydrogencarbonate | 18.76 g (18.76 %) |
[Reference example 2]
KI, KIO
3, dextrin, and citric anhydride were mixed, not by
using Flow Coater, in the following weight ratio (mixing
ratio of KI to KIO
3 = 6:1).
KI | 84.3 mg (23.06 %) |
KIO3 | 14.1 mg (3.86 %) |
Dextrin | 167.2 mg (45.75 %) |
Citric anhydride | 100.0 mg (27.36 %) |
[Reference example 3]
KI, KIO
3, dextrin, and citric anhydride were mixed, not by
using Flow Coater, in the following weight ratio (mixing
ratio of KI to KIO
3 = 8:1).
KI | 112.4 mg (25.46 %) |
KIO3 | 14.1 mg (3.19 %) |
Dextrin | 215.0 mg (48.70 %) |
Citric anhydride | 100.0 mg (27.36 %) |
[Stability test]
The stability test was performed as described below by
using the above examples of the present invention and
reference examples.
First of all, a 1g portion each was taken from the mixed
powders obtained in Example 1 of the present invention
and reference example 1, and placed in a transparent-glass
sample bottle (a volume of 15 mL). As for the examples 2
to 8 of the present invention and the reference examples 2
and 3, the same amount of each as described above was
placed in a transparent-glass sample bottle (a volume of 5
mL). These bottles were closed with plastic caps, wrapped
with parafilm, and stored in an incubator maintained at
50°C. On day 1 (example 1 of the present invention and
reference example 1) or day 5 (examples 2 to 6 of the
present invention and reference examples 2 and 3) of
storage, the color was visually observed, and possible
iodine release was also examined.
The criteria for the color change and iodine release are as
follows:
Color change
- ○:
- unchanged
- ▵:
- white → yellowish white or pale violet
- X:
- white → brown to black
Iodine release
- ○:
- iodine not released
- X:
- iodine released
The results on day 1 of storage are shown in Table 1, and
those on day 5, in Table 2.
No. | Color change | Iodine release |
Example 1 of the present invention | ○ | ○ |
Reference example 1 | ▵ | X |
No. | Color change | Iodine release |
Example 2 of the present invention | ▵ | ○ |
Example 3 of the present invention | ○ | ○ |
Example 4 of the present invention | ○ | ○ |
Example 5 of the present invention | ○ | ○ |
Example 6 of the present invention | ▵ | ○ |
Example 7 of the present invention | ○ | ○ |
Example 8 of the present invention | ○ | ○ |
Reference example 2 | X | X |
Reference example 3 | X | X |
As shown in Tables 1 and 2, the examples of the present
invention were accompanied by neither (or little) color
change nor iodine release whereas in the reference
examples, marked color changes as well as iodine release
were observed.
In order to confirm that iodine had not been inactivated in
the examples of the present invention, the samples were
dissolved in water after the test was completed. As a
result, the color changed into brown, and the peculiar odor
of iodine was generated. Thus, it was confirmed that
iodine existed availably without inactivation.
EXAMPLE 2 (water solubility test and antibacterial
activity test)
The examples 9 to 11 of the present invention and the
reference examples 4 and 5 were prepared according to the
following methods.
[Example 9 of the present invention]
750 g fine powder of povidone-iodine (the content of
available iodine is 11.4 % of complex of
polyvinylpyrrolidone and iodine, Nippo Kagaku) and 1750 g
fine powder of dextrin (Pinedex #3, Matsutani Kagaku
Kogyo) were placed in a testing Flow Coater,, and prepared
povidone-iodine/dextrin granulated powder containing
povidone-iodine and dextrin in a weight ratio of 30:70
(example 9 of the present invention) by the following
granulation conditions.
[Granulation conditions]
Temperature of blast inlet |
85°C |
Temperature of blast outlet |
50°C |
Wind delivery pressure |
150 mmHg |
Mixing time |
5 minutes |
Time for and frequency of water spraying |
2 minutes and 30 seconds each, 7 times (amount of water spraying 500 mL/7 times) |
Time for and frequency of interim-drying |
1 minute and 10 seconds each, 6 times |
Time for finish-drying |
3 minutes |
[Example 10 of the present invention]
The components were processed in the same manner as
described in the example 9 of the present invention, except
that the amount used was 1000 g for fine powder of
povidone-iodine and 1500 g for fine powder of dextrin, and
obtained a granulated powder containing povidone-iodine
and dextrin in a ratio of 40:60 (example 10 of the present
invention).
[Example 11 of the present invention]
The components were processed in the same manner as
described in the example 9 of the present invention, except
that the amount used was 1250 g for fine powder of
povidone-iodine and 1250 g for fine powder of dextrin, and
obtained a granulated powder containing povidone-iodine
and dextrin in a weight ratio of 50:50 (example 11 of the
present invention).
[Reference example 4]
The components were processed in the same manner as
described in the example 9 of the present invention, except
that 2500 g fine powder of povidone-iodine was used
without dextrin, and obtained a granulated powder
containing 100% povidone-iodine (reference example 4).
[Reference example 5]
750 g fine powder of povidone-iodine and 1750 g fine
powder of dextrin were placed in the testing henschel
mixer, mixed for 3 minites, and prepared
povidone-iodine/dextrin granulated powder containing
povidone-iodine and dextrin in a weight ratio of 30:70
(reference example 5).
Each sample obtained in this manner was tested for water
solubility and antibacterial activity as described below.
[Water solubility]
A 100 g portion of each sample was added into 100 mL
water, and stirred gently, and then allowed to stand. The
time required for its complete dissolution was measured.
[Antibacterial activity]
The minimum bactericidal concentration (MBC) of each
sample was measured as described below.
Each of 2 kinds of test strain suspension [E. coli (IFM
3039, 5.6 × 108 cells/mL) and MRSA (NTP 2019, 9.0 × 108
cells/mL) was incubated in tryptic soy broth (BBL) at 37°C
for 24 hours, and used as the inoculum. Each sample was
diluted with water using 2-fold serial dilutions, and used
as test solutions.
To each of 10 mL aliquots of these test solutions, 0.1-mL of
the inoculum was added, allowed to react for 1 minute, and
then iodine remaining in the solution was inactivated by
adding an equal volume of 1% sodium thiosulfate aqueous
solution. A 0.2-mL aliquot of the inactivated solution was
added to 10 mL tryptic soy broth, and incubated at 37°C
for 72 hours, and then it was evaluated visually by
observing the degree of turbidity of the medium whether
the bacterial growth occurred or not.
The results are shown in Table 3.
Samples | Water solubility | Antibacterial activity (MBC) |
| | E. coli | MRSA |
Example 9 of the present invention | Within 2 minutes | 260 ppm | 500 ppm |
Example 10 of the present invention | Within 3 minutes | 195 ppm | 375 ppm |
Example 11 of the present invention | Within 5 minutes | 130 ppm | 250 ppm |
Reference example 4 | 10 hours or more | 65 ppm | 125 ppm |
Reference example 5 | About 2 hours | 260 ppm | 500 ppm |
The results shown in Table 3 show that the examples 9 to
11 of the present invention were superior in water
solubility as well as in antibacterial activity against E.
coli and MRSA.
Industrial Applicability
The present invention was able to efficiently provide a
single-type solid preparation of iodophor which is stable
because of the composition as described above, releases no
iodine even if it is stored at a high temperature, and can
rapidly be dissolved before use.